CN210045055U - Ozone dehumidification equipment - Google Patents
Ozone dehumidification equipment Download PDFInfo
- Publication number
- CN210045055U CN210045055U CN201920814692.1U CN201920814692U CN210045055U CN 210045055 U CN210045055 U CN 210045055U CN 201920814692 U CN201920814692 U CN 201920814692U CN 210045055 U CN210045055 U CN 210045055U
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- Prior art keywords
- ozone
- drying
- dehumidification
- pipeline
- air
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 126
- 238000007791 dehumidification Methods 0.000 title claims abstract description 56
- 238000001035 drying Methods 0.000 claims abstract description 140
- 238000010438 heat treatment Methods 0.000 claims abstract description 56
- 238000009833 condensation Methods 0.000 claims abstract description 28
- 230000005494 condensation Effects 0.000 claims abstract description 28
- 238000006243 chemical reaction Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 17
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 17
- 239000001110 calcium chloride Substances 0.000 claims description 17
- 238000001816 cooling Methods 0.000 claims description 17
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
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- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses an ozone dehumidification equipment, including drying cabinet (1) and ozone generator (2), drying cabinet (1) through air duct (3) with ozone generator (2) intercommunication, air duct (3) are close to ozone generator's (2) one end is provided with drying valve (4) and drying fan (5), the middle part of air duct (3) still communicates there is the air guide branch pipe, the air guide branch pipe has set gradually electric heater (8), heating fan (7) and heating valve (6) from the outside inboard. The utility model discloses after ozone generator has generated ozone, still carry out condensation and drying process with ozone and for the air of reaction, further guaranteed the dryness fraction of ozone.
Description
Technical Field
The utility model belongs to the technical field of gaseous dehumidification, concretely relates to ozone dehumidification equipment.
Background
An ozone generator is a device for producing ozone gas. Ozone is easy to decompose and cannot be stored, and the ozone needs to be prepared and used on site, so that ozone generators are needed to be used in places where the ozone can be used, and the ozone generators are widely applied in the fields of drinking water, sewage, industrial oxidation, food processing and fresh keeping, medicine synthesis, space sterilization and the like, and are very important environment-friendly equipment. Ozone is soluble in water, and the solubility of ozone in water is about 13 times higher than that of oxygen and 25 times higher than that of air under normal temperature and normal pressure, so that the existing ozone generator is not suitable for being installed in a space with high air humidity, and the density of ozone is higher than that of air, so that ozone sinks in air. In the prior art, the ozone generator generates ozone by using air, but a large amount of water vapor exists in the air, and even if the air generates partial ozone in the ozone generator, the partial ozone is still accompanied with other components in the air and the water vapor, so that after the ozone generator generates the ozone, the partial ozone needs to be subjected to dehumidification treatment.
Therefore, an ozone dehumidifying apparatus is required.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide an ozone dehumidification device, when dry air needs to be fed into an ozone generator, an air guide branch pipe in the middle of an air guide pipe needs to be closed, namely a heating valve is closed, a heating fan does not act, and an electric heater does not act; at the moment, the drying valve is opened, the drying fan acts, and air directly enters the ozone generator through the air duct after being dried by the drying box; when the drying box needs to be reversely dehumidified, the drying valve needs to be closed, and the drying fan does not act; at the moment, the heating valve is opened, the heating fan acts, the electric heater acts, heat flow enters the drying box through the air guide branch pipe and the air guide pipe, and the calcium chloride drying net which absorbs a large amount of moisture in the drying box is reversely dried and dehumidified; after the ozone generator generates ozone, the ozone and the air for reaction are condensed and dried, so that the dryness of the ozone is further ensured.
In order to achieve the above object, the utility model adopts the following technical scheme:
an ozone dehumidification device comprises a drying box and an ozone generator, wherein the drying box is used for drying air used for producing reaction ozone, the ozone generator is used for generating ozone, the drying box is communicated with the ozone generator through an air guide pipe, a drying valve and a drying fan are arranged at one end, close to the ozone generator, of the air guide pipe, the middle of the air guide pipe is also communicated with an air guide branch pipe, and an electric heater, a heating fan and a heating valve are sequentially arranged on the air guide branch pipe from the outermost side to the inner side;
when dry air needs to be fed into the ozone generator, the air guide branch pipe in the middle of the air guide pipe needs to be closed, namely the heating valve is closed, the heating fan does not act, and the electric heater does not act; at the moment, the drying valve is opened, the drying fan acts, and air directly enters the ozone generator through the air duct after being dried by the drying box.
When the drying box needs to be reversely dehumidified, the drying valve needs to be closed, and the drying fan does not act; at the moment, the heating valve is opened, the heating fan acts, the electric heater acts, heat flow enters the drying box through the air guide branch pipe and the air guide pipe, and the calcium chloride drying net which absorbs a large amount of moisture in the drying box is dried and dehumidified reversely.
The ozone generator is divided into an ozone generating area and an ozone dehumidifying area; the ozone generating area is internally provided with an air inlet pipeline, a reaction chamber, an air outlet fan and an air outlet pipeline, and the air guide pipe is communicated with the reaction chamber through the air inlet pipeline; ozone dehumidification district is provided with the dehumidification admission line, dehumidification admission fan, cooling pipeline, condensation duct, drying chamber, heating motor and the dehumidification pipeline of giving vent to anger, the dehumidification admission line, condensation duct, drying chamber, the dehumidification pipeline of giving vent to anger communicate in proper order, give vent to anger the pipeline with the dehumidification admission line intercommunication, the cooling pipeline set up in the condensation duct is peripheral, the dehumidification admission fan sets up on the dehumidification admission line, the heating motor is right the drying chamber heating.
Air after the drying enters the reaction chamber from the air inlet pipeline to generate a certain amount of ozone, the ozone and the air are mixed together to enter the condensation pipeline and the drying chamber, and the dehumidification work of the ozone can be completed after condensation and drying, so that the dryness of the ozone is ensured.
Preferably, a plurality of layers of calcium chloride drying nets are arranged in the drying box, and a water outlet pipe is arranged at the bottom end of the drying box. The calcium chloride drying net can absorb a large amount of moisture in the air, and the more the layers of the calcium chloride drying net are, the larger the absorbed moisture is, and the drier the air is; when the water absorbed by the calcium chloride drying net is enough to form water drops, the water drops can be discharged through the water outlet pipe.
Preferably, a plurality of layers of drying blades are arranged in the drying chamber, and a plurality of air holes are formed in the drying blades. The arrangement of the plurality of layers of drying blades can increase the contact area between ozone and unreacted air and the drying blades, so that the efficiency is increased, and the air holes in the drying blades can facilitate the air circulation.
Preferably, the bottom of the condensation pipeline is provided with a drainage valve, and a drainage pipeline is installed at the drainage valve. The water condensed out of the ozone and unreacted air in the condenser pipe can open a drain valve and be discharged through a drain pipe.
Preferably, the top of the cooling pipeline is provided with a cold water inlet pipe, and the bottom of the cooling pipeline is provided with a cold water outlet pipe. Flowing cold water is introduced into the cooling pipeline, so that the cooling effect is ensured.
Preferably, still include humidity transducer, temperature sensor, flow rate sensor, signal comparator, first relay and second relay, the signal comparator respectively with humidity transducer, temperature sensor, flow rate sensor, first relay and second relay are connected, first relay with drying blower connects, the second relay is connected with electric heater and heating blower respectively, humidity transducer set up in inside the drying cabinet, temperature sensor set up in heating blower department, flow rate sensor set up in the air duct is close to ozone generator's one end. The method comprises the steps that humidity data detected by a humidity sensor are sent to a signal comparator, the signal comparator judges whether the humidity data exceed humidity threshold data, when the humidity data exceed the humidity threshold data, a drying valve needs to be closed, a drying fan does not act, a heating valve is opened, the heating fan acts, an electric heater acts, heat flow enters a drying box through an air guide branch pipe and an air guide pipe, and reverse drying dehumidification is carried out on a calcium chloride drying net absorbing a large amount of moisture in the drying box; the temperature sensor detects temperature data of the heating fan, when the signal comparator judges that the temperature data exceeds a threshold temperature, the heating valve is closed, the heating fan does not act, and the electric heater does not act; the flow velocity sensor detects the flow velocity of the air in the air guide pipe, when the signal comparator judges that the flow velocity data exceeds the threshold flow velocity, the drying valve needs to be closed, the drying fan does not act, and the problem that the ozone generator cannot work normally due to overlarge flow velocity is avoided.
Preferably, the condensation pipe is a spiral condensation pipe. The spiral-type condensation pipe can increase the condensation time of the ozone and the unreacted air, so that the ozone and the moisture in the unreacted air are fully condensed.
Preferably, the ozone generating zone is not located above the ozone dehumidification zone. The ozone generator is disposed above the dehumidifying structure because of its high ozone density and air.
The utility model has the beneficial technical effects that: (1) when dry air needs to be fed into the ozone generator, the air guide branch pipe in the middle of the air guide pipe needs to be closed, namely the heating valve is closed, the heating fan does not act, and the electric heater does not act; at the moment, the drying valve is opened, the drying fan acts, and air directly enters the ozone generator through the air duct after being dried by the drying box; when the drying box needs to be reversely dehumidified, the drying valve needs to be closed, and the drying fan does not act; at the moment, the heating valve is opened, the heating fan acts, the electric heater acts, heat flow enters the drying box through the air guide branch pipe and the air guide pipe, and the calcium chloride drying net which absorbs a large amount of moisture in the drying box is reversely dried and dehumidified; after the ozone generator generates ozone, the ozone and the air for reaction are condensed and dried, so that the dryness of the ozone is further ensured.
(2) The method comprises the steps that humidity data detected by a humidity sensor are sent to a signal comparator, the signal comparator judges whether the humidity data exceed humidity threshold data, when the humidity data exceed the humidity threshold data, a drying valve needs to be closed, a drying fan does not act, a heating valve is opened, the heating fan acts, an electric heater acts, heat flow enters a drying box through an air guide branch pipe and an air guide pipe, and reverse drying dehumidification is carried out on a calcium chloride drying net absorbing a large amount of moisture in the drying box; the temperature sensor detects temperature data of the heating fan, when the signal comparator judges that the temperature data exceeds a threshold temperature, the heating valve is closed, the heating fan does not act, and the electric heater does not act; the flow velocity sensor detects the flow velocity of air in the air guide pipe, and when the signal comparator judges that the flow velocity data exceeds the threshold flow velocity, the drying valve needs to be closed, the drying fan does not act, the phenomenon that the ozone generator cannot work normally due to overlarge flow velocity is avoided, and the safety of the device is ensured.
Drawings
Fig. 1 is a schematic structural diagram of an embodiment of the present invention.
Fig. 2 is a schematic structural diagram of an ozone generator according to an embodiment of the present invention.
Fig. 3 is a schematic structural view of an ozone dehumidification region according to an embodiment of the present invention.
Fig. 4 is a schematic circuit diagram of an embodiment of the present invention.
Wherein, the drying box 1
Drying valve 4
Drying fan 5
Calcium chloride drying net 9
Dehumidification air inlet pipe 203
Dehumidification air inlet fan 204
Drain pipe 208
Dehumidification gas outlet pipe 213
Cold water inlet pipe 217
A cold water delivery line 218.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to fig. 1-4 of the present invention, and it should be apparent that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Example (b):
as shown in fig. 1, an ozone dehumidification device comprises a drying box 1 and an ozone generator 2, wherein the drying box is used for drying air for producing reaction ozone, the ozone generator is used for generating ozone, the drying box 1 is communicated with the ozone generator 2 through an air duct 3, one end, close to the ozone generator 2, of the air duct 3 is provided with a drying valve 4 and a drying fan 5, the middle part of the air duct 3 is also communicated with an air guide branch pipe, and the air guide branch pipe is sequentially provided with an electric heater 8, a heating fan 7 and a heating valve 6 from the outermost side to the inner side;
when dry air needs to be fed into the ozone generator, the air guide branch pipe in the middle of the air guide pipe needs to be closed, namely the heating valve is closed, the heating fan does not act, and the electric heater does not act; at this time, the drying valve is opened, the drying fan is operated, and the air directly enters the ozone generator through the air duct after passing through the air inlet pipe 10 to the drying box for drying.
When the drying box needs to be reversely dehumidified, the drying valve needs to be closed, and the drying fan does not act; at the moment, the heating valve is opened, the heating fan acts, the electric heater acts, heat flow enters the drying box through the air guide branch pipe and the air guide pipe, and the calcium chloride drying net which absorbs a large amount of moisture in the drying box is dried and dehumidified reversely.
As shown in fig. 2 and 3, the ozone generator 2 is divided into an ozone generating region and an ozone dehumidifying region; wherein, an air inlet pipeline 202, a reaction chamber 201, an air outlet fan 214 and an air outlet pipeline 216 are arranged in the ozone generation area, and the air duct 3 is communicated with the reaction chamber 201 through the air inlet pipeline 202; ozone dehumidification district is provided with dehumidification admission line 203, dehumidification inlet fan 204, cooling tube 205, condensation duct 206, drying chamber 210, heating motor 212 and dehumidification outlet pipe 213, dehumidification admission line 203, condensation duct 206, drying chamber 210, dehumidification outlet pipe 213 communicate in proper order, outlet pipe 216 with dehumidification admission line 203 intercommunication, cooling tube 205 set up in condensation duct 206 is peripheral, dehumidification inlet fan 204 sets up on the dehumidification inlet pipe 203, heating motor 212 is right drying chamber 210 heats.
Air after the drying enters the reaction chamber from the air inlet pipeline to generate a certain amount of ozone, the ozone and the air are mixed together to enter the condensation pipeline and the drying chamber, and the dehumidification work of the ozone can be completed after condensation and drying, so that the dryness of the ozone is ensured.
Preferably, a plurality of layers of calcium chloride drying nets 9 are arranged inside the drying box 1, and a water outlet pipe 11 is arranged at the bottom end of the drying box 1. The calcium chloride drying net can absorb a large amount of moisture in the air, and the more the layers of the calcium chloride drying net are, the larger the absorbed moisture is, and the drier the air is; when the water absorbed by the calcium chloride drying net is enough to form water drops, the water drops can be discharged through the water outlet pipe.
Preferably, a plurality of layers of drying blades 209 are arranged in the drying chamber 210, and a plurality of air holes 211 are formed in the drying blades 209. The arrangement of the plurality of layers of drying blades can increase the contact area between ozone and unreacted air and the drying blades, so that the efficiency is increased, and the air holes in the drying blades can facilitate the air circulation.
Preferably, a drain valve 207 is arranged at the bottom of the condensation pipeline 206, and a drain pipe 208 is arranged at the drain valve 207. The water condensed out of the ozone and unreacted air in the condenser pipe can open a drain valve and be discharged through a drain pipe.
Preferably, a cold water inlet pipe 217 is arranged at the top of the cooling pipeline 205, and a cold water outlet pipe 218 is arranged at the bottom of the cooling pipeline 205. Flowing cold water is introduced into the cooling pipeline, so that the cooling effect is ensured.
As shown in fig. 4, preferably, the ozone drying device further comprises a humidity sensor, a temperature sensor, a flow rate sensor, a signal comparator, a first relay and a second relay, wherein the signal comparator is respectively connected with the humidity sensor, the temperature sensor, the flow rate sensor, the first relay and the second relay, the first relay is connected with the drying fan 5, the second relay is respectively connected with the electric heater and the heating fan, the humidity sensor is arranged inside the drying box 1, the temperature sensor is arranged at the heating fan 7, and the flow rate sensor is arranged at one end of the air duct 3 close to the ozone generator 2. The method comprises the steps that humidity data detected by a humidity sensor are sent to a signal comparator, the signal comparator judges whether the humidity data exceed humidity threshold data, when the humidity data exceed the humidity threshold data, a drying valve needs to be closed, a drying fan does not act, a heating valve is opened, the heating fan acts, an electric heater acts, heat flow enters a drying box through an air guide branch pipe and an air guide pipe, and reverse drying dehumidification is carried out on a calcium chloride drying net absorbing a large amount of moisture in the drying box; the temperature sensor detects temperature data of the heating fan, when the signal comparator judges that the temperature data exceeds a threshold temperature, the heating valve is closed, the heating fan does not act, and the electric heater does not act; the flow velocity sensor detects the flow velocity of the air in the air guide pipe, when the signal comparator judges that the flow velocity data exceeds the threshold flow velocity, the drying valve needs to be closed, the drying fan does not act, and the problem that the ozone generator cannot work normally due to overlarge flow velocity is avoided.
Preferably, the condensation duct 206 is a spiral-type condensation duct. The spiral-type condensation pipe can increase the condensation time of the ozone and the unreacted air, so that the ozone and the moisture in the unreacted air are fully condensed.
Preferably, the ozone generating zone is not located above the ozone dehumidification zone. The ozone generator is disposed above the dehumidifying structure because of its high ozone density and air.
In the description of the present invention, it should be understood that the terms "counterclockwise", "clockwise", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description of the present invention, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.
Claims (8)
1. The ozone dehumidification equipment is characterized by comprising a drying box (1) and an ozone generator (2), wherein the drying box (1) is communicated with the ozone generator (2) through an air duct (3), one end, close to the ozone generator (2), of the air duct (3) is provided with a drying valve (4) and a drying fan (5), the middle of the air duct (3) is also communicated with an air guide branch pipe, and the air guide branch pipe is sequentially provided with an electric heater (8), a heating fan (7) and a heating valve (6) from the outermost side to the inner side;
the ozone generator (2) is divided into an ozone generating area and an ozone dehumidifying area; the ozone generating device comprises an ozone generating area, a gas inlet pipeline (202), a reaction chamber (201), a gas outlet fan (214) and a gas outlet pipeline (216), wherein the gas guide pipe (3) is communicated with the reaction chamber (201) through the gas inlet pipeline (202); ozone dehumidification district is provided with dehumidification admission line (203), dehumidification admission fan (204), cooling pipeline (205), condensation pipeline (206), drying chamber (210), heating motor (212) and the dehumidification pipeline of giving vent to anger (213), dehumidification admission line (203), condensation pipeline (206), drying chamber (210), the dehumidification pipeline of giving vent to anger (213) communicate in proper order, give vent to anger pipeline (216) with dehumidification admission line (203) intercommunication, cooling pipeline (205) set up in condensation pipeline (206) are peripheral, dehumidification admission fan (204) set up on the dehumidification admission line (203), heating motor (212) are right drying chamber (210) heating.
2. The ozone dehumidification device as claimed in claim 1, wherein a plurality of layers of calcium chloride drying nets (9) are arranged inside the drying box (1), and a water outlet pipe (11) is arranged at the bottom end of the drying box (1).
3. The ozone dehumidification device as claimed in claim 1, wherein a plurality of layers of drying blades (209) are disposed in the drying chamber (210), and a plurality of air holes (211) are formed on the drying blades (209).
4. The ozone dehumidification device as claimed in claim 1, wherein a drain valve (207) is disposed at a bottom of the condensation pipeline (206), and a drain pipeline (208) is disposed at the drain valve (207).
5. The ozone dehumidification device according to claim 1, wherein a cold water inlet pipe (217) is arranged at the top of the cooling pipe (205), and a cold water outlet pipe (218) is arranged at the bottom of the cooling pipe (205).
6. The ozone dehumidification equipment as claimed in claim 1, further comprising a humidity sensor, a temperature sensor, a flow rate sensor, a signal comparator, a first relay and a second relay, wherein the signal comparator is respectively connected with the humidity sensor, the temperature sensor, the flow rate sensor, the first relay and the second relay, the first relay is connected with the drying fan (5), the second relay is respectively connected with the electric heater (8) and the heating fan (7), the humidity sensor is arranged inside the drying box (1), the temperature sensor is arranged at the heating fan (7), and the flow rate sensor is arranged at one end of the air duct (3) close to the ozone generator (2).
7. An ozone dehumidification apparatus as in claim 1 wherein said condensation duct (206) is a spiral condensation duct.
8. The ozone dehumidification apparatus according to claim 1, wherein said ozone generating region is not located above said ozone dehumidification region.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920814692.1U CN210045055U (en) | 2019-05-31 | 2019-05-31 | Ozone dehumidification equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920814692.1U CN210045055U (en) | 2019-05-31 | 2019-05-31 | Ozone dehumidification equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210045055U true CN210045055U (en) | 2020-02-11 |
Family
ID=69396743
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920814692.1U Expired - Fee Related CN210045055U (en) | 2019-05-31 | 2019-05-31 | Ozone dehumidification equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN210045055U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114993028A (en) * | 2022-06-17 | 2022-09-02 | 广东高景太阳能科技有限公司 | Silicon wafer drying treatment method and system |
-
2019
- 2019-05-31 CN CN201920814692.1U patent/CN210045055U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114993028A (en) * | 2022-06-17 | 2022-09-02 | 广东高景太阳能科技有限公司 | Silicon wafer drying treatment method and system |
| CN114993028B (en) * | 2022-06-17 | 2023-05-30 | 高景太阳能股份有限公司 | Silicon wafer drying treatment method and system |
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| GR01 | Patent grant | ||
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200211 |